TW517068B - Fiber-reinforced composite and method of making same - Google Patents
Fiber-reinforced composite and method of making same Download PDFInfo
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- TW517068B TW517068B TW87110640A TW87110640A TW517068B TW 517068 B TW517068 B TW 517068B TW 87110640 A TW87110640 A TW 87110640A TW 87110640 A TW87110640 A TW 87110640A TW 517068 B TW517068 B TW 517068B
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- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04C—STRUCTURAL ELEMENTS; BUILDING MATERIALS
- E04C5/00—Reinforcing elements, e.g. for concrete; Auxiliary elements therefor
- E04C5/07—Reinforcing elements of material other than metal, e.g. of glass, of plastics, or not exclusively made of metal
- E04C5/073—Discrete reinforcing elements, e.g. fibres
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B15/00—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00
- B29B15/08—Pretreatment of the material to be shaped, not covered by groups B29B7/00 - B29B13/00 of reinforcements or fillers
- B29B15/10—Coating or impregnating independently of the moulding or shaping step
- B29B15/12—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length
- B29B15/122—Coating or impregnating independently of the moulding or shaping step of reinforcements of indefinite length with a matrix in liquid form, e.g. as melt, solution or latex
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C70/00—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts
- B29C70/04—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts comprising reinforcements only, e.g. self-reinforcing plastics
- B29C70/28—Shaping operations therefor
- B29C70/40—Shaping or impregnating by compression not applied
- B29C70/50—Shaping or impregnating by compression not applied for producing articles of indefinite length, e.g. prepregs, sheet moulding compounds [SMC] or cross moulding compounds [XMC]
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/04—Reinforcing macromolecular compounds with loose or coherent fibrous material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2075/00—Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24058—Structurally defined web or sheet [e.g., overall dimension, etc.] including grain, strips, or filamentary elements in respective layers or components in angular relation
- Y10T428/24124—Fibers
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/249921—Web or sheet containing structurally defined element or component
- Y10T428/249924—Noninterengaged fiber-containing paper-free web or sheet which is not of specified porosity
- Y10T428/24994—Fiber embedded in or on the surface of a polymeric matrix
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/249921—Web or sheet containing structurally defined element or component
- Y10T428/249924—Noninterengaged fiber-containing paper-free web or sheet which is not of specified porosity
- Y10T428/24994—Fiber embedded in or on the surface of a polymeric matrix
- Y10T428/249942—Fibers are aligned substantially parallel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/249921—Web or sheet containing structurally defined element or component
- Y10T428/249924—Noninterengaged fiber-containing paper-free web or sheet which is not of specified porosity
- Y10T428/24994—Fiber embedded in or on the surface of a polymeric matrix
- Y10T428/249942—Fibers are aligned substantially parallel
- Y10T428/249944—Fiber is precoated
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Architecture (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Structural Engineering (AREA)
- Civil Engineering (AREA)
- Composite Materials (AREA)
- Reinforced Plastic Materials (AREA)
- Manufacture Of Alloys Or Alloy Compounds (AREA)
Abstract
Description
517068 經漓部中泱標準局!工消费合作社印製 A7 B7 五、發明説明(i ) 本發明係關於纖維加強複合物。已知經由於拉塑裝置 拉伸^維,使用樹脂浸潰纖維及同時於加熱模具内成形及 固化結構件而生產纖維強化複合物之方法(參考聚合物科 學工程百科,第二版第4卷,約翰威利父子公司,紐約,丨_28 頁,1986年)。因有效樹脂浸潰需要低熔體黏度(複合物可 接受性質之必要要求),熱固物比熱塑材料更佳。雖然熱 固複合物具有絕佳機械性質但有若干缺點:熱固基體之伸 長率有限,熱固前驅物為非期望的揮發性有機化合物或來 源,複合物無法再度成形或回收,及其生產速率受限。 近年來,致力於使用熱塑材料製造複合物。例如, Hawley於美國專利4,439,387教示經由埋置纖維之模具擠 塑稼融熱塑樹脂材料。於美國專利4,559,262,〇0§_611等 揭示纖維強化組合物,其係經由連續拉伸多條纖維通過浸 /貝浴獲得’浸潰浴為具有夠低分子量(結果導致低溶體黏 度)可充份濕潤纖維之熱塑聚合物靜態熔體組成。c〇gaweU 專教示之適當聚合物包括熱塑聚酯類,聚醯胺類,聚颯類 ,聚氧亞甲基類,聚丙烯,聚伸芳基硫化物類,聚環氧苯 /聚笨乙稀攙合物’聚_喊鋼類及聚醚酮類。C〇gSweu等 也教示為了於強化組合物可達成接受的物理性質,較佳熔 體黏度超過1 Ns/m2。如此,若熱塑樹脂分子量夠低而達 成夠低溶體黏度來加工處理樹脂,則所得表合物之性質受 損。 單層纖維強化片(或帶)之厚度受先前技術方法所限。 例如,Cogswell等教示單層帶厚度約〇1毫米(21攔,29至31 紙張尺度適州中國國家標埤(CNS) A^m~( 210x797^1 ) --:- !丨——0—r (請先閱讀背面之注意事項再填寫本頁)517068 Zhongli Standard Bureau of the Ministry of Economic Affairs! Printed by the Industrial and Consumer Cooperatives A7 B7 V. Description of the Invention (i) The present invention relates to fiber-reinforced composites. It is known to produce fiber-reinforced composites by stretching dimensional fiber in a drawing device, using resin to impregnate fibers, and simultaneously forming and curing structural parts in a heated mold (refer to the Encyclopedia of Polymer Science and Engineering, Second Edition, Volume 4) John Wiley & Sons, New York, p. 28, 1986). Because effective resin impregnation requires low melt viscosity (a necessary requirement for the acceptable properties of the composite), thermosets are better than thermoplastic materials. Although the thermoset composite has excellent mechanical properties, it has several disadvantages: the elongation of the thermoset matrix is limited, the thermoset precursor is an undesired volatile organic compound or source, the composite cannot be reshaped or recycled, and its production rate Restricted. In recent years, efforts have been made to make composites using thermoplastic materials. For example, U.S. Patent No. 4,439,387 to Hawley teaches extruding crops to melt thermoplastic resin materials through a mold in which fibers are embedded. In U.S. Patent No. 4,559,262, 00§_611, etc., a fiber-reinforced composition is disclosed. The fiber-reinforced composition is obtained by continuously drawing a plurality of fibers through a dipping / shell bath. The dipping bath is sufficiently low in molecular weight (resulting in low solution viscosity). Parts of thermoplastic polymer static melt composition of wet fiber. 〇gaweU Appropriately taught polymers include thermoplastic polyesters, polyamides, polyfluorenes, polyoxymethylenes, polypropylenes, polyarylene sulfides, polyepoxybenzene / polybenzyl Ethylene admixtures' poly_steel and polyetherketones. CogSweu et al. Also teach that in order to achieve acceptable physical properties of the reinforcing composition, a preferred melt viscosity of more than 1 Ns / m2. As such, if the molecular weight of the thermoplastic resin is sufficiently low to achieve a sufficiently low solution viscosity to process the resin, the properties of the resulting surface compound are impaired. The thickness of the single-layer fiber-reinforced sheet (or tape) is limited by the prior art methods. For example, Cogswell et al. Teach that the thickness of a single-layer belt is about 0.01 mm (21 bar, 29 to 31 paper size, China State Standard (CNS) A ^ m ~ (210x797 ^ 1)----! 丨 ——0— r (Please read the notes on the back before filling this page)
、1T 4, 1T 4
五、發明説明(3 ) 經濟部中央標準局員工消费合作社印紫 月曰’及至少30%容積比由聚合物樹脂浸潰之強化纖維延伸 貫穿$長度’但纖維長度大於100毫米及具有單層厚度至 少約0.2毫米。 第二態樣中,本發明為一種製備纖維強化剛性熱塑聚 胺基甲酸酯複合物之方法,該方法包括下列步驟:將纖維 束連續拉伸通過熔體,該熔體係經由加熱含有水解穩定性 及熱穩定性催化劑之剛性熱塑聚胺基甲酸酯至足夠解聚合 熱塑聚胺基甲酸酯之溫度獲得;使用解聚合熱塑聚胺基甲 、酸S旨浸潰經拉伸纖維束而形成複合熔體;將複合熔體成形 為厚度至少0.2毫米之物件;然後冷卻複合物熔體而再聚 合熱塑聚胺基甲酸酯,其中該纖維組成複合物總容積之至 少50容積%。 第二悲樣中’本發明為一種改良之藉拉塑製備纖維強 化複合物之方法,該方法包括以聚合物熔體浸潰纖維束之 步驟,改良部份包含熔體流過大體具有縱向長槽適合纖維 束於炫體流之橫向方向通過之加熱導管;及纖維束通過長 槽,故熔體大體完全寖潰纖維束。· 本發明經由提供於升高溫度具有夠低熔體黏度之熱塑 物而有效浸潰纖維束且無需限制熱塑物分子量。本發明之 較佳態樣中,經由纖維接觸熱熔體流動流可免除聚合物熔 體之熱貯器需求。如此,減少聚合物之非也望的劣化。 第1圖為用於製備纖維強化熱塑複合物之較佳拉塑機/ 擠塑機裝置之示意圖。 第2圖為拉塑機/擠塑機裝置之浸潰單元及壓密單元之 本紙張尺度適州中國國家標埤((、NS ) Λ4規格(2】〇X297公釐) (請先閱讀背面之注意事項再填寫本負) I# ,ιτ •Γ 6 517068 經濟部中央標牟局貞工消贽合作社印製 A7 __________B7五、發明説明(4 ) ' 分解示圖。 巧3圖為浸潰針之側視圖。 第4圖為拭除板之較佳設計。 可解聚合且可再聚合熱塑聚合物(DRTp)可藉任何適 當手段,較佳藉業界眾所周知之擠塑方法浸潰於纖維束而 形成纖維強化複合物。較佳,浸潰方法係使用根據第1圖 示例說明之方法使用纖維拉塑及聚合物樹脂熔體擠塑之組 合進行。需了解,該方法可用於使用任一種可流動之樹脂 =,非僅DRTP浸潰纖維束。 現在參照第1圖,來自纖維備料(12)之纖維束(1〇)被拉 送通過纖維預熱站(14),及含有紅外線陶瓷加熱器。纖維 束(10)可由任何多種不同類型材料包括玻璃,碳,聚芳醯 胺纖維,陶瓷及多種金屬組成。預熱站夠熱而可去除任何 存在於纖維之水,及預熱纖維至高於樹脂熔體固化點之溫 度。然後纖維束(10)拉送通過纖維預拉張單元(16),其為 針陣列將各別纖維展開且使其處於張力下,然後拉送通過 浸潰單元(18),於此處纖維束以樹脂熔體濕潤。 樹脂熔體較佳以下述方式製備。固體樹脂經造粒,然 後於除濕器(24)内乾燥至不多於2〇〇 ppm水,更佳不多於 100 ppm水。然後除濕後之粒狀樹脂較佳擠塑通過經加熱 的單螺桿擠塑機(26),其藉剪切及加熱熔4樹脂。然後樹 脂炫體利用經加熱的樹脂槽道(28)轉運至浸潰單元(18)。 現在參照第2圖,浸潰單元(18)含有至少一根浸潰針 (20)及系列桿(22)。浸潰針(20)包含一根大體筒形件(30), 本紙張尺度適州中國國家標啤(CNS ) Λ4規格(2ΐ〇χ297公釐) (請先閲讀背面之注意事項再填寫本頁) L0V. Explanation of the invention (3) The consumer cooperative of the Central Standards Bureau of the Ministry of Economic Affairs of the People's Republic of China printed Ziyue Yue and at least 30% of the volume ratio of the fiber reinforced fiber impregnated with polymer resin extends through $ length, but the fiber length is greater than 100 mm and has a single layer The thickness is at least about 0.2 mm. In a second aspect, the present invention is a method for preparing a fiber-reinforced rigid thermoplastic polyurethane composite. The method includes the steps of continuously stretching a fiber bundle through a melt, and the melt system contains hydrolysis by heating. Stability and heat stability catalyst rigid thermoplastic polyurethane is obtained to a temperature sufficient to depolymerize thermoplastic polyurethane; using depolymerized thermoplastic polyurethane, acid S to immerse and pull Extending the fiber bundle to form a composite melt; forming the composite melt into an object having a thickness of at least 0.2 mm; and then cooling the composite melt to repolymerize the thermoplastic polyurethane, wherein the fibers constitute at least the total volume of the composite 50% by volume. In the second example, the present invention is an improved method for preparing a fiber-reinforced composite by drawing plastic. The method includes the step of impregnating a fiber bundle with a polymer melt. The groove is suitable for the heating duct through which the fiber bundle passes in the transverse direction of the body stream; and the fiber bundle passes through the long groove, so the melt is substantially completely impregnated with the fiber bundle. · The present invention effectively impregnates fiber bundles by providing a thermoplastic having a sufficiently low melt viscosity at elevated temperatures without limiting the molecular weight of the thermoplastic. In a preferred aspect of the present invention, the need for a thermal reservoir for the polymer melt is eliminated by contacting the hot melt flow with the fibers. In this way, unexpected degradation of the polymer is reduced. FIG. 1 is a schematic diagram of a preferred stretcher / extruder device for preparing a fiber-reinforced thermoplastic composite. Figure 2 shows the paper size of the dipping unit and the compaction unit of the drawing machine / extrusion machine. The paper size is in accordance with the state standard of China ((, NS) Λ4 (2) × 297mm) (Please read the back first) (Notes should be filled out again) I #, ιτ • Γ 6 517068 Printed by A7 __________ B7 of the Central Standards Bureau of the Ministry of Economic Affairs, Zhengong Consumer Cooperative V. 5. Description of the invention (4) 'Exploded view. Coincidentally, the figure 3 is an immersion needle Side view. Figure 4 shows the preferred design of the wipe board. The depolymerizable and repolymerizable thermoplastic polymer (DRTp) can be immersed in the fiber bundle by any suitable means, preferably by extrusion methods known in the industry. A fiber-reinforced composite is formed. Preferably, the impregnation method is performed using a combination of fiber drawing and polymer resin melt extrusion according to the method illustrated in Figure 1. It should be understood that this method can be used for any Flowable resin =, not only DRTP impregnated fiber bundles. Now referring to Figure 1, the fiber bundle (10) from the fiber preparation (12) is pulled through the fiber preheating station (14), and contains infrared ceramic heating The fiber bundle (10) can be made by any of many different types Materials include glass, carbon, polyaramide fibers, ceramics, and various metals. The preheating station is hot enough to remove any water present in the fibers, and preheat the fibers to a temperature above the solidification point of the resin melt. Then the fiber bundles (10) Pull through the fiber pre-tensioning unit (16), which is an array of needles to unwind the individual fibers under tension, and then pull through the impregnation unit (18), where the fiber bundle is melted with resin The resin melt is preferably prepared in the following manner. The solid resin is granulated and then dried in a dehumidifier (24) to not more than 200 ppm water, more preferably not more than 100 ppm water. After dehumidification The granular resin is preferably extruded through a heated single-screw extruder (26), which melts the 4 resin by shearing and heating. The resin body is then transferred to the impregnation unit using the heated resin channel (28). (18). Referring now to Figure 2, the impregnation unit (18) contains at least one impregnation needle (20) and a series of rods (22). The impregnation needle (20) includes a generally cylindrical member (30), This paper is suitable for China National Standard Beer (CNS) Λ4 size (2 × 〇297mm) ( (Please read the notes on the back before filling out this page) L0
、1T 鲁! 7 517068 怒濟部中次標準局負,τ消f合作社印製 A7 B7 五、發明説明(5 ) 且含有· a)兩條縱向槽道,第一槽道供轉運樹脂熔體(32) ,及子二槽道供匣式加熱器(34),加熱器可維持浸潰針(2〇) 加熱至高於樹脂熔點之溫度,或於DRTP之例高於解聚合 溫度,較佳於200。〇至約300°C之範圍;及b)經由安裝細長 件(36)南於浴第一槽道(32)重合之浸潰針(2〇)之縱向開口 形成長槽。於浸潰針(20)頂部之縱向開口可提供樹脂熔體 接觸纖維束之手段,纖維束以相對於流過第一槽道之樹脂 熔體流之橫向方向拉伸通過長槽。熔體與纖維束之接觸闡 明於第2圖之(38)。 需了解“頂部開口,,僅為方便使用而絕非意圖限制浸潰 針的設計。此外,形成纖維束(1〇)可通過其中且與樹脂接 觸之長槽可以多種方式進行,例如於縱向方向研磨中空圓 柱。 於纖維束(10)拉送通過浸潰針(2〇)之長槽且以樹脂熔 體濕潤後,濕纖維束(1Ga)經由-系列濕桿(22)編織而辅助 樹脂的浸潰。浸潰妥的纖維束(1〇a)被拉送通過壓密單元 (40),該單元含有一個模具(42),其初步成形纖維束(i〇a) ,及含有多片拭除板(44),其進一步將纖維束(1〇a)成形為 所需物件並去除過量熔體,及隨後改良浸潰。各片拭除板 (44)有個開口具有待成形之部件形狀。開口尺寸與浸潰單 兀(16)之更為下游變成縮小,至達到期望▲形的剖面尺寸 為止。第4圖示例說明拭除板(44)之較佳設計。 •再度參照第1圖,複合物區段被拉送通過冷卻模具(4〇 ,其固㈣體且提供光滑表面。冷卻模具(46)設計成具有 I紙張尺€巾_ 家料(( 210X297^11~ ----- (請先閲讀背面之注意事項再填寫本頁), 1T Lu! 7 517068 The Ministry of Nucai ’s Intermediate Standards Bureau was negative, τ 消 f co-operative printed A7 B7 V. Description of the invention (5) and contains · a) two longitudinal channels, the first channel is for transferring the resin melt (32), And the two-channel cassette-type heater (34), the heater can maintain the immersion needle (20) to be heated to a temperature higher than the melting point of the resin, or higher than the depolymerization temperature in the case of DRTP, preferably 200. A range of 0 to about 300 ° C; and b) a long groove is formed through the longitudinal opening of the immersion needle (20) which is superposed on the first channel (32) of the bath with the elongated member (36) south. The longitudinal opening at the top of the impregnation needle (20) provides a means for the resin melt to contact the fiber bundle, and the fiber bundle is stretched through the long groove in a lateral direction relative to the resin melt flow through the first channel. The contact between the melt and the fiber bundle is illustrated in Figure 2 (38). It should be understood that "the top opening is only for convenience and is not intended to limit the design of the immersion needle. In addition, the formation of long grooves through which the fiber bundle (10) can pass and contact the resin can be performed in various ways, such as in the longitudinal direction Grind the hollow cylinder. After the fiber bundle (10) is drawn through the long groove of the impregnation needle (20) and wet with the resin melt, the wet fiber bundle (1Ga) is woven through the series wet rod (22) to assist the resin. Impregnation. The impregnated fiber bundle (10a) is drawn through a compaction unit (40), which contains a mold (42) that initially shapes the fiber bundle (ioa) and contains multiple wipes. The removing plate (44) further shapes the fiber bundle (10a) into a desired object and removes excess melt, and then improves the impregnation. Each piece of the erasing plate (44) has an opening with the shape of the part to be formed The opening size and the immersion unit (16) are further reduced downstream until they reach the desired ▲ -shaped cross-sectional size. Figure 4 illustrates the preferred design of the wiper plate (44) by example. • Refer to Figure 1 again Figure, the composite section is pulled through the cooling mold (40, its solid body and lifting Smooth surface. Cooling the mold (46) designed to have a paper size I € _ home towel material ((210X297 ^ 11 ~ ----- (Read Notes on the back and then fill the page)
、1T I -1 i - · 517068 Α7 Β7 五、發明説明( 待成形物件尺寸。完成之物件較佳藉毛蟲型拖戈機(48)來 拉送]大體彼此對正平行之纖維係占已完成之纖維強化複 合件總容積至少約30容積%,較佳至少約50容積%,及更 佳至少約65容積%,及加強纖維大體延伸貫穿複合物全長 。經拉塑段可切成任一種所需長度,由數毫米至數千米, 及進一步使用業界眾所周知之技術成形,成型,或接合, 包括熱成形,熱衝鍛,及熔接。出乎意外地,本發明之較 佳方法提供製備具有單層厚度至少〇·2毫米,較佳至少1毫 米,更佳至少2¾米,及最佳至少5毫米之手段。 纖維強化複合物聚合物之較佳類別為加熱時解聚合及 冷部時再聚合之熱塑聚合物。此種熱塑聚合物之範例包括 具如下結構單位之聚合物: ----------- (請先閲讀背面之注意事項再填寫本頁) 訂 —Z—C—NH- 經濟部中央標準局貞工消费合作社印製 其中Z為S或0,較佳〇,及2,為3,〇,N•烧基或顺, 佳0或NH,更佳〇。較佳DRTp為熱塑聚胺基甲酸酯類 熱塑聚脲類,較佳熱塑聚胺基甲酸酯類。 DRTP為單向或二向聚合物其可經由適當化學計算 之下列各者反應製備:a)二異氰酸酯或二異硫氰酸酯,較 佳二異氰酸酯;b)含有兩個活性氫基之低分子量化合物( 不大於300道耳吞),及c)選擇性含有兩個活性氫基之高分 子量化合物(分子量通常於約500至約8,000道耳吞之範圍) 。低分子量化合物組合二異氰酸酯或二異硫氰酸酯,促成 及 量 9 5l7〇68 經?0部中决標準局貞工消费合作社印製 Α7 Β7 五、發明説明(7 ) %做“硬段”内容物’及高分子量化合物組合二異氰酸自旨咬 ~異硫氣酸Si,組成所谓之軟段”内容物。、 1T I -1 i-· 517068 Α7 Β7 V. Description of the invention (size of the object to be formed. The completed object is preferably pulled by a caterpillar-type towing machine (48)]. The fiber lines that are generally parallel to each other have been completed. The total volume of the fiber-reinforced composite part is at least about 30% by volume, preferably at least about 50% by volume, and more preferably at least about 65% by volume, and the reinforcing fibers generally extend through the entire length of the composite. The stretched plastic section can be cut into any type Required length, from a few millimeters to several kilometers, and further formed, shaped, or joined using techniques well known in the industry, including hot forming, hot stamping, and welding. Surprisingly, the preferred method of the present invention provides The thickness of a single layer is at least 0.2 mm, preferably at least 1 mm, more preferably at least 2¾ meters, and most preferably at least 5 mm. The preferred types of fiber-reinforced composite polymers are depolymerization during heating and re-cooling. Polymerized thermoplastic polymer. Examples of such thermoplastic polymers include polymers with the following structural units: ----------- (Please read the notes on the back before filling this page) Order — Z—C—NH- in the Ministry of Economic Affairs Printed by the Standard Bureau of Zhenggong Consumer Cooperatives where Z is S or 0, preferably 0, and 2 as 3, 0, N • A or cis, preferably 0 or NH, more preferably 0. The preferred DRTp is a thermoplastic polymer Urethanes are thermoplastic polyureas, preferably thermoplastic polyurethanes. DRTP is a unidirectional or bidirectional polymer that can be prepared by the reaction of each of the following suitable chemical calculations: a) diisocyanate or diisocyanate Isothiocyanate, preferably diisocyanate; b) a low molecular weight compound containing two active hydrogen groups (not more than 300 channels) and c) a high molecular weight compound optionally containing two active hydrogen groups (typically molecular weight In the range of about 500 to about 8,000 ear swallows). The combination of low molecular weight compounds of diisocyanate or diisothiocyanate, and the amount of 0 Partially printed standard printed by Zhengong Consumer Cooperative A7 B7 V. Description of the invention (7)% do "hard segment" content 'and high molecular weight compound combination diisocyanate intentionally bite ~ isosulfuric acid Si, composition The so-called "soft segment" content.
I 如此處使用“活性氫基”一詞表示可與異氰酸根或異硫 氰酸根反應之基如所示··I As used herein, the term "active hydrogen group" means a group that can react with isocyanate or isothiocyanate as shown ...
R.-ZH + R-NCZ ——-R.-Z-LnH—R 其中Z及Z,定義如前,及R及R,為連接基,可為脂族、芳 族或脂環族或其組合。 〈 含兩個活性氫之化合物可為二醇,二胺,二硫醇,經 胺,硫醇胺,或羥硫醇,較佳為二硫醇。 DRTP可為剛性或軟性。軟DRTP較佳熱塑聚胺基甲酸 酯(STPUs)之特徵為具有蕭耳A硬度不大於95或&不大於 25 C。剛性DRTP較佳為剛性熱塑聚胺基甲酸酯(RTpUs), 具有玻璃化溫度(Tg)不大於50 °C及典型具有硬段含量至少 75 /〇。RTPUs之揭示及製備例如由G〇idwasser等述於美國 專利4,376,834。RTPUs為本發明複合物,較佳熱塑聚合物 。市售RTPIJs範例包括IS0PLASTi程用熱塑聚胺基甲酸 酯類(陶氏化學公司商品名)。 較佳二異氰酸酯類包括芳族、脂族、及脂環族二異氰 酉文酉曰及其組合。較佳二異氰酸酯類之代表例參考美國專利 4’3 85,133,4,522,975;及5,167,899。較佳彳二異氰酸醋包 括4,4’_二異氰酸根二苯基甲烷,對_伸苯基二異氰酸酯, I,3貳(異氰酸根甲基)環己烷,i,4_二異氰酸根環己烷, /、亞甲基一異氰酸酯,伸萘基二異氰酸酯,3,3,_二甲 (請先閱讀背面之注意事項再填寫本頁) 訂 10 517068 經满部中决標準局貞工消费合作社印製 Α7 Β7 五、發明説明(8 ) 基_4,4’-聯苯二異氰酸酯,4,4,-二異氰酸根二環己基甲烷 ,及2,4-伸甲笨二異氰酸酯。更佳為4,4、二異氰酸根二環 己基曱烷及4,4,二異氰酸根二苯基甲烷。最佳為4,4,_二異 氰酸根二笨基甲燒。 較佳含兩個活性氫基之低分子量化合物為乙二醇, 1,3-丙二醇’ 1,4_丁二醇,ι,5-戊二醇,丨士己二醇,二乙 二醇,三乙二醇,三丙二醇,四乙二醇,新戊二醇,^4-環己二醇,1,4-環己烷二甲醇,丨/兴貳羥乙基)氫醌,2,2_ 貳(β-羥-4-乙氧苯基)丙烷(亦即,乙氧化雙酚A)及其混合 物。較佳鏈延長劑為Μ-丁二醇,l56_己二醇,Μ_環己烷 二曱醇,二乙二醇,三乙二醇,三丙二醇及其混合物。 DRTP可選擇性含有由含兩個活性氫基之高分子量化 合物形成的結構單位,較佳為分子量係於較佳不低於約750 ’更佳不低於約1〇〇〇,及最佳不低於約15〇〇 ;及較佳不高 於約6000,及更佳不高於約5〇〇〇之範圍之二醇。高分子量 二醇之單位係占DRTP較佳RTPU之夠低分量,故DRTP之Tg 南於50°C。較佳,高分子量二醇單位·係占RTPU之不多於 約25 ’更佳不多於約丨〇及最佳不多於約5重量%,至約〇重 量 %RTPU 〇 高分子量二醇較佳為聚酯二醇或聚醚二醇或其組合。 較佳聚醋二醇及聚醚二醇類之範例包括聚色内酯二醇,聚 氧伸乙基二醇,聚氧伸丙基二醇,聚氧四亞甲基二醇,聚 伸乙基己二酸酯,聚伸丁基己二酸酯二醇,聚伸乙基_伸 丁基己二酸酯二醇及聚(六亞甲基碳酸酯二醇),或其組合 本紙張人度速川中國國彖標埤((、NS ) Μ規格(21〇 X 297公釐) (請先閱讀背面之注意事項再填寫本頁)R.-ZH + R-NCZ ——- R.-Z-LnH—R where Z and Z are as defined above, and R and R are linking groups, which can be aliphatic, aromatic or cycloaliphatic or combination. The compound containing two active hydrogens may be a diol, a diamine, a dithiol, an amine, a thiolamine, or a hydroxythiol, and preferably a dithiol. DRTP can be rigid or soft. Soft DRTP preferred thermoplastic polyurethanes (STPUs) are characterized by having a Shore A hardness of not more than 95 or & 25 C. The rigid DRTP is preferably a rigid thermoplastic polyurethane (RTpUs), has a glass transition temperature (Tg) of not more than 50 ° C, and typically has a hard segment content of at least 75 / 〇. The disclosure and preparation of RTPUs are described, for example, by Goidwasser et al. In U.S. Patent 4,376,834. RTPUs are compounds of the present invention, preferably thermoplastic polymers. Examples of commercially available RTPIJs include thermoplastic polyurethanes for the ISOPLASTi process (trade name of The Dow Chemical Company). Preferred diisocyanates include aromatic, aliphatic, and cycloaliphatic diisocyanates, and combinations thereof. Representative examples of preferred diisocyanates are referenced in U.S. Patents 4'3 85,133,4,522,975; and 5,167,899. Preferred diisocyanates include 4,4'-diisocyanatodiphenylmethane, p-phenylene diisocyanate, I, 3 '(isocyanatomethyl) cyclohexane, i, 4_ Diisocyanate cyclohexane, /, methylene monoisocyanate, naphthyl diisocyanate, 3,3, _dimethyl (Please read the precautions on the back before filling this page) Order 10 517068 Printed by Standard Bureau of Zhenggong Consumer Cooperatives A7 B7 V. Description of the invention (8) 4-4,4'-biphenyl diisocyanate, 4,4, -diisocyanate dicyclohexylmethane, and 2,4-methylene Stupid diisocyanate. More preferred are 4,4, diisocyanatodicyclohexylfluorane and 4,4, diisocyanatodiphenylmethane. The most preferred is 4,4, _diisocyanate. Preferred low-molecular-weight compounds containing two active hydrogen groups are ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, hexylene glycol, diethylene glycol, Triethylene glycol, tripropylene glycol, tetraethylene glycol, neopentyl glycol, ^ 4-cyclohexanediol, 1,4-cyclohexanedimethanol, // hydroxyethyl) hydroquinone, 2,2_ Samarium (β-hydroxy-4-ethoxyphenyl) propane (ie, ethoxylated bisphenol A) and mixtures thereof. Preferred chain extenders are M-butanediol, 156-hexanediol, M_cyclohexanediethanol, diethylene glycol, triethylene glycol, tripropylene glycol, and mixtures thereof. DRTP may optionally contain a structural unit formed of a high molecular weight compound containing two active hydrogen groups, preferably having a molecular weight of preferably not less than about 750 ′, more preferably not less than about 1,000, and most preferably Diols below about 15,000; and preferably no higher than about 6000, and more preferably no higher than about 5,000. The units of high molecular weight diols are low enough for DRTP's better RTPU, so the Tg of DRTP is 50 ° C. Preferably, the high molecular weight diol unit is no more than about 25 'of the RTPU, more preferably no more than about 丨 0, and most preferably no more than about 5% by weight, to about 0% by weight RTPU. It is preferably a polyester diol or a polyether diol or a combination thereof. Examples of preferred polyglycol glycols and polyether glycols include polylactone glycol, polyoxyethylene glycol, polyoxypropylene glycol, polyoxytetramethylene glycol, polyethylene glycol Adipate, polybutylene adipate diol, polyethylene adipate and poly (hexamethylene carbonate diol), or a combination thereof Du Suchuan China National Standard ((, NS) M specifications (21 × 297 mm) (Please read the precautions on the back before filling in this page)
、1T 11 517068 經濟部中央標準局男工消费合作社印製 A7 B7 五、發明説明(9 ) 〇 今應物之異氰酸根對XH,較佳〇H比由約〇.95 : 1, 較佳0.975 : 1,及更佳由約〇·985 : 1至約1 〇5 : 1,較佳約 1.025 : 1,及更佳約 1.015 : 1。 DRTP,較佳RTPU可優異地於有效量之水解穩定性及 熱穩定性催化劑存在下製備,該催化劑可催化異氰酸基與 活性氫基間之反應,活性氫基較佳為羥基,反應形成胺基 曱酸酯,脲,或硫腺鍵聯,較佳胺基甲酸酯鍵聯,且於聚 合物解聚合過程中保持活性而催化胺基曱酸酯、脲或硫脲 間鍵結再度形成,較佳為胺基曱酸醋鍵結之再度形成並重 建分子量。此等催化劑範例為Sn+2例如辛酸亞錫;及sn+4 催化劑如二烷基錫二硫醇鹽類,較佳二甲基錫二硫醇鹽( 可以FOMREZ UL-22,Witco化學公司商品名獲得),及二 烧基錫二羧酸鹽,如美國專利3,661,887詳細揭示者。較 佳,催化劑之存在量占反應物重量約〇·〇〇丨至約5重量0/〇。 非為DRTP之熱塑樹脂可與DRTP併用而製造本發明之 複合物,但非DRTP之用量夠低故樹脂之熔體黏度保持夠 低而可有效浸潰纖維束。非DRTP之範例包括丙烯腈-丁二 烯·乙烯共聚物類,聚苯乙烯類,聚伸苯基氧化物,聚伸 笨基氧化物聚苯乙烯攙合物,聚氧亞曱基類,聚丙稀,聚 醯胺類,聚伸丁基對酞酸酯,聚(伸乙基森酞酸酯),聚( 伸丁基對酞酸酯)與聚(伸乙基對酞酸酯)之聚酯共聚物, 苯乙.烯-乙婦腈共聚物,及乙婦-丙稀-二烯三聚物。 複合物也包括添加劑如阻燃劑,紫外光安定劑,顏料 本紙張尺度述州中國國家標準(CNS ) Λ4規格(210X 297公釐) (請先閱讀背面之注意事項再填寫本頁)1T 11 517068 Printed by A7 B7, Male Workers' Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (9) 〇 The isocyanate pair XH of the present application should preferably be 〇H ratio from about 0.95: 1, better 0.975: 1, and more preferably from about 0.8985: 1 to about 105: 1, more preferably about 1.025: 1, and more preferably about 1.015: 1. DRTP, preferably RTPU, can be prepared excellently in the presence of an effective amount of hydrolytic and thermal stability catalysts, which can catalyze the reaction between an isocyanate group and an active hydrogen group. The active hydrogen group is preferably a hydroxyl group, which forms Urethane, urea, or thiogland linkages, preferably urethane linkages, which remain active during polymer depolymerization and catalyze the re-bonding between the urethane, urea, or thiourea Formation, preferably re-formation of the amino acetic acid bond and re-establishing molecular weight. Examples of such catalysts are Sn + 2 such as stannous octoate; and sn + 4 catalysts such as dialkyltin dithiolates, preferably dimethyltin dithiolates (available in FOMREZ UL-22, a product of Witco Chemical Company) (Namely obtained), and dialkyltin dicarboxylate, as disclosed in detail in U.S. Patent 3,661,887. More preferably, the catalyst is present in an amount of from about 0.000 to about 5 weight 0 / 〇. Non-DRTP thermoplastic resin can be used in combination with DRTP to make the composite of the present invention, but the amount of non-DRTP is low enough so that the melt viscosity of the resin is kept low enough to effectively impregnate the fiber bundles. Examples of non-DRTP include acrylonitrile-butadiene · ethylene copolymers, polystyrenes, polyphenylene oxides, polystyrene oxide polystyrene compounds, polyoxymethylene groups, polypropylene Dilute, polyamines, polybutylene terephthalate, poly (butylene terephthalate), poly (butylene terephthalate) and poly (ethylene terephthalate) Ester copolymers, styrene-ethylene-acetonitrile copolymers, and ethene-propylene-diene terpolymers. The compound also includes additives such as flame retardants, UV stabilizers, and pigments. This paper is described in the state Chinese National Standard (CNS) Λ4 specification (210X 297 mm) (Please read the precautions on the back before filling this page)
、1T f 12 517068 A7 '------- B7 五、發明説日^ ~ ,染料,抗靜電劑,.抗微生物劑,殺真菌劑,去霉劑及流 動促進劑。 \ (請先閱讀背面之注意事項再填寫本頁) 強化熱塑複合物可由DRTP製備其比較由非可解聚合 及再聚合熱塑物製備之複合物具有出乎意外之優異物理性 夤此外,使用drtp,特別使用較佳裝置需可快速拉送 速率,較佳至少約1米/分鐘,更佳至少約2米/分鐘,更佳 至少約5米/分鐘,及最佳至少約1〇米/分鐘,而未犧牲浸 潰程度。較佳複合物具有抗彎強度至少5〇〇 Mpa,更佳至 少750 MPa,及最佳至少i2〇〇MPa,即使使用玻璃纖維亦 如此。遠更高的強度可使用聚芳醯胺及碳纖維達成。 本發明之強化複合物可用於廣泛多種需要極高強度及 剛性’以及額外敏密之用途,例如雪展,滑雪撐桿,诡系覽 ,帳蓬柱,混凝土,防衝撞之護攔,門或窗框,纜索及光 纖纜索。 下列實例僅供舉例說明之用,而非意圖限制本發明之 範圍。 經濟部中戎標率局1只工消贽合作社印製 實例-浸潰以剛性熱塑聚胺基甲酸酯之·玻璃纖維之製備 24束纖維(歐文康寧公司,R43S,2400特)排列成3層 ,拉送通過240°C之預熱站。ISOPAST 2530聚胺基甲酸g旨 工程用熱塑樹脂(陶氏化學公司商品名)已經於皮歐文除濕 乾燥器内於95°C預熱超過8小時及於柯林4單螺桿擠塑機 加工處理(螺桿速度25 rpm,筒段溫度250°C(料斗),260°C ,及270°C)。連桿設定於280°C。各層纖維拉送通過浸潰 針,於此處纖維飽和以聚胺基甲酸酯熔體然後通過若干熱 本Λ尺㊈J1]中國國家標潭(CNS ) ( 21〇X 297^f ) ~ -13 - 517068 A7 -________ Β7 五、發明説明(u ) 才干編織。浸潰針之各自長槽尺寸為高〇·8毫米,寬6〇毫米 ,第了槽道長120毫米及槽道直徑30毫米。浸潰針維持285 °C,其它桿維持於260°C。纖維拉伸速率為2米/分鐘。生 產尺寸為2釐米寬x2毫米厚(及長度可變)之長條。纖維強 化複合物之抗彎強度為1300 MPa,及抗彎模量為41 GPa(BS 2787測試)。 元件標號對照 4〇···纖維束 30.··筒形件 12…纖維備料 32…第一槽道 14…纖維預熱站 3 4…第二槽道 16···纖維預拉張單元 3 6 · · ·細長件 1 8…浸潰單元 3 8…接點 2〇…浸潰針 40…壓密單元 22…桿 42…模具 24.··除濕器 44···拭除板 26…單螺桿擠塑機 46···冷卻模具 28…槽道 48.··毛蟲型拖曳機 (請先閲讀背面之注意事項再填寫本頁)、 1T f 12 517068 A7 '------- B7 V. The day of invention ^ ~, dyes, antistatic agents, antimicrobial agents, fungicides, mold removers and flow promoters. \ (Please read the precautions on the back before filling this page) Reinforced thermoplastic composites can be prepared by DRTP, which has unexpectedly superior physical properties compared to composites made from non-decomposable polymerized and repolymerized thermoplastics. Additionally, The use of drtp, especially the preferred device, requires a fast pull rate, preferably at least about 1 m / min, more preferably at least about 2 m / min, more preferably at least about 5 m / min, and most preferably at least about 10 m Per minute without sacrificing the degree of impregnation. Preferably, the composite has a flexural strength of at least 500 Mpa, more preferably at least 750 MPa, and most preferably at least 200 MPa, even when glass fibers are used. Much higher strength can be achieved using polyaramide and carbon fibers. The reinforced composites of the present invention can be used in a wide variety of applications that require extremely high strength and rigidity, as well as extra sensitivity, such as snow shows, ski poles, parasols, tent posts, concrete, anti-collision barriers, doors or Window frames, cables and fiber optic cables. The following examples are for illustrative purposes only and are not intended to limit the scope of the invention. An example printed by the China Industrial Standards Bureau of the Ministry of Economic Affairs and a cooperative—the impregnation with rigid thermoplastic polyurethane · glass fiber made of 24 bundles of fibers (Owen Corning Corporation, R43S, 2400 Te) 3 layers, pulled through 240 ° C preheating station. ISOPAST 2530 Polyurethane G thermoplastic resin (Dow Chemical Co., Ltd.) has been preheated in a Pirwin desiccant dryer at 95 ° C for more than 8 hours and processed on a Colin 4 single screw extruder (Screw speed 25 rpm, barrel temperature 250 ° C (hopper), 260 ° C, and 270 ° C). The connecting rod is set at 280 ° C. Each layer of fiber is pulled through the impregnation needle, where the fiber is saturated with polyurethane melt and then passes through a number of thermal books Λ ㊈ ㊈ J1] China National Standard Pool (CNS) (21〇X 297 ^ f) ~ -13 -517068 A7 -________ Β7 V. Description of the invention (u) Talent weaving. The dimensions of the respective long grooves of the impregnated needle are 0.8 mm in height and 60 mm in width. The length of the first groove is 120 mm and the diameter of the groove is 30 mm. The immersion needle was maintained at 285 ° C, and the other rods were maintained at 260 ° C. The fiber draw rate was 2 meters / minute. Production of strips measuring 2 cm wide x 2 mm thick (and variable length). The fiber-reinforced composite has a flexural strength of 1300 MPa and a flexural modulus of 41 GPa (tested by BS 2787). Comparison of component numbers 40. Fiber bundles 30. Cylindrical pieces 12 ... Fiber preparation 32 ... First channel 14 ... Fiber preheating station 3 4 ... Second channel 16 ... Fiber pretensioning unit 3 6 · · · Slim pieces 1 8… immersion unit 3 8… contact 2… immersion needle 40… compaction unit 22… rod 42… mold 24… dehumidifier 44… wipe plate 26… single Screw extruder 46 ... Cooling mold 28 ... Channel 48 ... Caterpillar towing machine (Please read the precautions on the back before filling this page)
、1T .1 經濟部中央標準局吳工消费合作社印製 本紙張尺度適用中國國家標缚((、奶)/\4規格(210'/ 297公釐) 14、 1T .1 Printed by Wu Gong Consumer Cooperative, Central Bureau of Standards, Ministry of Economic Affairs This paper size applies to China's national standard ((, milk) / \ 4 size (210 '/ 297 mm) 14
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US08/888,340 US5891560A (en) | 1997-07-02 | 1997-07-02 | Fiber-reinforced composite and method of making same |
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TW517068B true TW517068B (en) | 2003-01-11 |
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US (2) | US5891560A (en) |
EP (1) | EP0993487B8 (en) |
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AT (1) | ATE294832T1 (en) |
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CA (1) | CA2294963A1 (en) |
DE (1) | DE69830056T2 (en) |
TW (1) | TW517068B (en) |
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- 1997-07-02 US US08/888,340 patent/US5891560A/en not_active Expired - Lifetime
-
1998
- 1998-06-09 AT AT98928932T patent/ATE294832T1/en not_active IP Right Cessation
- 1998-06-09 JP JP50715499A patent/JP2002508021A/en active Pending
- 1998-06-09 EP EP19980928932 patent/EP0993487B8/en not_active Expired - Lifetime
- 1998-06-09 WO PCT/US1998/011826 patent/WO1999001501A2/en not_active Application Discontinuation
- 1998-06-09 CA CA 2294963 patent/CA2294963A1/en not_active Abandoned
- 1998-06-09 KR KR1019997012560A patent/KR20010014389A/en not_active Application Discontinuation
- 1998-06-09 BR BR9810497A patent/BR9810497A/en active Search and Examination
- 1998-06-09 DE DE1998630056 patent/DE69830056T2/en not_active Expired - Lifetime
- 1998-07-01 TW TW87110640A patent/TW517068B/en active
-
1999
- 1999-01-28 US US09/238,712 patent/US6165604A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
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US5891560A (en) | 1999-04-06 |
CA2294963A1 (en) | 1999-01-14 |
JP2002508021A (en) | 2002-03-12 |
US6165604A (en) | 2000-12-26 |
EP0993487A2 (en) | 2000-04-19 |
EP0993487B1 (en) | 2005-05-04 |
ATE294832T1 (en) | 2005-05-15 |
KR20010014389A (en) | 2001-02-26 |
EP0993487B8 (en) | 2005-06-29 |
WO1999001501A2 (en) | 1999-01-14 |
WO1999001501A3 (en) | 1999-03-25 |
DE69830056D1 (en) | 2005-06-09 |
DE69830056T2 (en) | 2006-01-19 |
BR9810497A (en) | 2001-12-26 |
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